US4740530A - Method for foaming synthetic resin bodies with microwave or high frequency energy - Google Patents
Method for foaming synthetic resin bodies with microwave or high frequency energy Download PDFInfo
- Publication number
- US4740530A US4740530A US07/091,970 US9197087A US4740530A US 4740530 A US4740530 A US 4740530A US 9197087 A US9197087 A US 9197087A US 4740530 A US4740530 A US 4740530A
- Authority
- US
- United States
- Prior art keywords
- slab
- microwave
- foaming
- synthetic resin
- high frequency
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000005187 foaming Methods 0.000 title claims abstract description 38
- 229920003002 synthetic resin Polymers 0.000 title claims abstract description 30
- 239000000057 synthetic resin Substances 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims description 13
- 229920005989 resin Polymers 0.000 claims abstract description 7
- 239000011347 resin Substances 0.000 claims abstract description 7
- 239000006260 foam Substances 0.000 claims description 12
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 11
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 11
- 239000000178 monomer Substances 0.000 claims description 10
- 239000004604 Blowing Agent Substances 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 9
- 230000005855 radiation Effects 0.000 claims description 9
- GYCMBHHDWRMZGG-UHFFFAOYSA-N Methylacrylonitrile Chemical compound CC(=C)C#N GYCMBHHDWRMZGG-UHFFFAOYSA-N 0.000 claims description 8
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 6
- 229920000642 polymer Polymers 0.000 claims description 6
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 5
- 150000002825 nitriles Chemical class 0.000 claims 3
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 8
- 239000004033 plastic Substances 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 229920001577 copolymer Polymers 0.000 description 4
- -1 Polyethylene Polymers 0.000 description 3
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 3
- 230000000977 initiatory effect Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 206010017076 Fracture Diseases 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- ATHHXGZTWNVVOU-UHFFFAOYSA-N N-methylformamide Chemical compound CNC=O ATHHXGZTWNVVOU-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- STVZJERGLQHEKB-UHFFFAOYSA-N ethylene glycol dimethacrylate Chemical compound CC(=C)C(=O)OCCOC(=O)C(C)=C STVZJERGLQHEKB-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229920007790 polymethacrylimide foam Polymers 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- BJELTSYBAHKXRW-UHFFFAOYSA-N 2,4,6-triallyloxy-1,3,5-triazine Chemical compound C=CCOC1=NC(OCC=C)=NC(OCC=C)=N1 BJELTSYBAHKXRW-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- 208000010392 Bone Fractures Diseases 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 208000013201 Stress fracture Diseases 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 229920003020 cross-linked polyethylene Polymers 0.000 description 1
- 239000004703 cross-linked polyethylene Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- DZBOAIYHPIPCBP-UHFFFAOYSA-L magnesium;2-methylprop-2-enoate Chemical compound [Mg+2].CC(=C)C([O-])=O.CC(=C)C([O-])=O DZBOAIYHPIPCBP-UHFFFAOYSA-L 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 1
- 229920003145 methacrylic acid copolymer Polymers 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical compound C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 description 1
- 125000002560 nitrile group Chemical group 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000012802 pre-warming Methods 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- FBCQUCJYYPMKRO-UHFFFAOYSA-N prop-2-enyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC=C FBCQUCJYYPMKRO-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
- B29C35/02—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
- B29C35/08—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/3415—Heating or cooling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/56—After-treatment of articles, e.g. for altering the shape
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
- B29C35/02—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
- B29C35/08—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation
- B29C35/0805—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation using electromagnetic radiation
- B29C2035/0855—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation using electromagnetic radiation using microwave
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
- B29C35/02—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
- B29C35/12—Dielectric heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2033/00—Use of polymers of unsaturated acids or derivatives thereof as moulding material
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S521/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S521/915—Utilizing electrical or wave energy during cell forming process
Definitions
- the present invention relates to a method for making a rigid foam article by prewarming a rigid heat-foamable synthetic resin until at least a portion of the resin surface is softened and then initiating the foaming process by further heating with microwave or high-frequency radiation.
- the prewarmed synthetic resin is a copolymer comprising at least 80 percent by weight of units of acrylic acid or methacrylic acid and of acrylonitrile or methacrylonitrile, together with a blowing agent. On heating, acrylimide or methacrylimide groups are formed from the acid and nitrile groups.
- uniform foam slabs are obtained in a microwave or high-frequency field if a rigid slab of foamable synthetic resin is preheated until at least a portion of its surface is at or above the softening temperature of the resin and the microwave or high-frequency field initiating the foaming process is then allowed to act on the slab until foaming occurs. It is important that a microwave or high-frequency field of an intensity that will induce foaming not be allowed to act on the foamable synthetic resin slab until at least a portion of its surface has been thermally softened. How it is heated is not important so long as this condition is satisfied. If preheating is effected by means of a microwave or high-frequency field, its intensity must be such that foaming will not set in.
- softening temperature is meant that temperature at which the synthetic resin elastically expands under the foaming pressure without fracturing.
- the temperature at which this condition occurs may be exceeded, but preferably not to the extent that the temperature region of plastic deformability is reached.
- any heat source with which the softening temperature can be reached at the surface is suitable for the preheating of the foamable synthetic-resin slab.
- an air oven in which an appropriately heated atmosphere, usually air, will act on the surface of the slab may be employed, or the slab surface may be exposed to heat radiation. Heating by heat transfer from a liquid medium or a hot solid surface is also possible but is usually less convenient.
- microwave fields or high-frequency fields can be used for preheating, alone or together with the other heat sources mentioned, provided that care is taken that foaming is not prematurely induced in the interior.
- a field of appropriately low intensity may be used or the field may be allowed to act on the slab only momentarily or intermittently.
- the microwave or high-frequency field adapted to induce foaming can be cut in. This is preferably done only when the surface of the synthetic resin slab has been heated completely or almost completely to or above the softening temperature. It is not detrimental if foaming has already set in at the surface. Further heating to foaming temperature is faster than with any other heat source acting only externally.
- Microwave ovens which are suitable for use in the method of the invention are known in the art, where they are employed for drying, for example. They operate with wavelengths ranging from 1 to 50 cm. The most commonly used wavelength is 12.3 cm, which corresponds to 2450 MHz.
- the radiation or field is produced by a so-called magnetron and is distributed in the microwave oven as uniformly as possible. The more uniform the field, the lower the danger that isolated foaming zones will form that are not associated with a softened surface zone.
- the power output of the microwave generator will, of course, have to be based on the size of the synthetic resin slab to be foamed and on the foaming temperature required.
- High frequency generators suitable for use in the method of the invention operate at wavelengths ranging from 1 to 50 meters.
- a commonly used wavelength is 11 meters, which corresponds to 27.12 MHz.
- Such generators are employed to heat-seal plastics and to foam wetted polystyrene beads.
- Kunststoff-Physik im Gespraech (“Discourse on the Physics of Synthetic Resins"), a publication of BASF AG, 1969, p. 179.)
- a field distribution that is as uniform as possible will be advantageous.
- a material In order that a material may be heated in a microwave or high-frequency field, it must be capable of absorbing the respective radiation. That will be the case of the material contains a sufficient number of polar structures. Such structures may be a constituent of the polymer molecules which make up the synthetic resin or they may be contained in low molecular weight substances, such as water or formamide, admixed with it. Synthetic resins having polar structures include those which contain carbonyl, carboxyl, hydroxyl, halogen, amino, or carboxylamido groups.
- synthetic resins containing a copolymer comprising at least 80 percent by weight of units of acrylic acid or methacrylic acid and of acrylonitrile or methacrylonitrile are suitable for use in the method of the inventions.
- the polymer should comprise at least 20 percent by weight of acrylic acid or methacrylic acid.
- the ratio by weight of acrylic acid and/or methacrylic acid to acrylonitrile and/or methacrylonitrile is from 3 : 2 to 2 : 3.
- the copolymer may contain up to 20 percent by weight of other ethylenically unsaturated monomers copolymerizable therewith, for example acrylamide and methacrylamide, styrene, lower alkyl (C 1 -C 4 ) esters of acrylic acid and methacrylic acid, as well as up to 5 percent by weight of crosslinking monomers having 2 or more polymerizable double bonds, such as esters of acrylic acid and methacrylic acid with polyols (e.g. glycol dimethacrylate), divinylbenylene, triallyl cyanurate, and methylene-bis-acrylamide.
- polyols e.g. glycol dimethacrylate
- divinylbenylene divinylbenylene
- triallyl cyanurate methylene-bis-acrylamide
- metal salts of acrylic acid and methacrylic acid may be present in amounts up to 5 percent by weight, particularly salts of polyvalent metal ions such as Mg 2+ , Zr 4+ , Cr 3+ , Co 2+ , Zn 2+ , Cd 2+ , Bi 3+ , TiO 2+ , and Pb 2+ .
- These synthetic resins soften at from 140° C. to 150° C. and start to foam from 160° C. to 180° C.
- a reaction of polymerized units of acrylonitrile or methacrylonitrile and units of acrylic or methacrylic acid takes place to form units of acrylimide or methacrylimide. Foamed plastics based on polymethacrylimide have acquired considerable commercial importance.
- such resins also comprise from 2 to 15 percent, preferably 2 to 10 percent, by weight of a blowing agent which on being heated yields a gas or vapor.
- a blowing agent which on being heated yields a gas or vapor.
- Formamide, monomethyl formamide, urea, water, and lower aliphatic alcohols are illustrative of such blowing agents, which are well known in the art.
- Slabs of such a synthetic resin having a thickness of from 1 to 4 cm, for example, are best heated in a circulating air oven at 170° C. to 200° C. until the surface softens and are then exposed to a microwave field. Preheating usually takes from about 5 to 30 minutes, while the microwave treatment requires somewhat less time. By contrast, when foaming is effected by the use of hot air alone, a foaming time of about 2 hours is required.
- a slab measuring 70 ⁇ 70 ⁇ 23 mm of a rigid foamable synthetic resin having a softening temperature of 160° C. and containing a copolymer of methacrylic acid and methacrylonitrile in a molar ratio of 3:2 together with 8 percent, by weight of the polymer, of a blowing agent mixture of formamide and tert.-butanol was preheated in a hot air oven to an approximately uniform surface temperature of 160° C. within 30 minutes and then treated for 6 minutes with a microwave field whose power was controlled through an operating cycle of 10 seconds of radiation followed by a 50-second pause.
- a foam slab naming a density of 38 kg/m 3 was so obtained.
- the microwave oven employed (Sharp Model R 8000 E) had a power consumption of 1.4 kw in the hot air section and of 1.3 kw in the microwave section, with a power output of 650 watts with a 2-liter water load, and had been retrofitted to permit simultaneous microwave and hot air operation. This made it possible to carry out the entire foaming operation in the same unit using only hot air during the preheating time and then cutting in microwave heating for foaming.
- a slab measuring 120 ⁇ 120 ⁇ 23 mm of a rigid foamable synthetic resin having a softening temperature of 180° C. and containing a weakly crosslinked copolymer of methacrylonitrile and methacrylic acid in the aforementioned molar proportions and 10 percent, by weight of the polymer, of a blowing agent mixture of formamide and tert-butanol was preheated for 30 minutes in a hot air oven to an approximately uniform surface temperature of 180° C.
- the preheated slab was placed between the electrodes if a high frequency furnace (Model HGV 4001 of the firm Herfurth GmbH) having a useful output of 4 kw at a frequency of 27.12 MHz.
- the electrodes measured 400 ⁇ 400 mm.
- a monomer mixture comprising:
- the prewarmed piece was foamed in 5-7 minutes in a high frequency field as in Example 2, during which 50 percent of maximum output was intermittently applied.
Landscapes
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Toxicology (AREA)
- Physics & Mathematics (AREA)
- Oral & Maxillofacial Surgery (AREA)
- Thermal Sciences (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Molding Of Porous Articles (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19863630930 DE3630930A1 (de) | 1986-09-11 | 1986-09-11 | Verfahren zur herstellung eines hartschaumstoffes mittels eines mikrowellen- oder hochfrequenzfeldes |
| DE3630930 | 1986-09-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4740530A true US4740530A (en) | 1988-04-26 |
Family
ID=6309364
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/091,970 Expired - Fee Related US4740530A (en) | 1986-09-11 | 1987-09-02 | Method for foaming synthetic resin bodies with microwave or high frequency energy |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US4740530A (de) |
| EP (1) | EP0259706B1 (de) |
| JP (1) | JPS6374629A (de) |
| DE (2) | DE3630930A1 (de) |
| ES (1) | ES2016601B3 (de) |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4840758A (en) * | 1988-09-09 | 1989-06-20 | Phillips Petroleum Company | Methods of preparing molded thermoplastic articles wherein radio frequency energy is utilized to heat the thermoplastic material |
| US4990539A (en) * | 1988-12-16 | 1991-02-05 | Basf Aktiengesellschaft | Preparation of styrene polymer foam particles |
| EP0978601A1 (de) * | 1998-08-05 | 2000-02-09 | Exploitatiemaatschappij Merode B.V. | Verfahren und Vorrichtung zur Herstellung eines isolierenden Elementes und damit hergestellter Elemente |
| NL1009885C2 (nl) * | 1998-08-18 | 2000-02-21 | Exploitatiemaatschappij Merode | Werkwijze en inrichting voor het vervaardigen van een isolatie-element, aldus verkregen isolatie-element en dakconstructie voorzien van één of meer isolatie-elementen. |
| US20040101674A1 (en) * | 2002-11-06 | 2004-05-27 | Leslie Ross | Composite sheet material |
| EP1332030A4 (de) * | 2000-08-14 | 2009-02-11 | Novamont Spa | Verfahren zum herstellen biologisch abbaubarer schaumprodukte |
| KR100943399B1 (ko) * | 2001-08-29 | 2010-02-22 | 에보니크 룀 게엠베하 | 폴리메타크릴이미드 발포체의 제조방법 및 당해 방법으로 수득 가능한 폴리메타크릴이미드의 발포 판 또는 시이트 |
| CN103524968A (zh) * | 2013-10-23 | 2014-01-22 | 江苏兆鋆新材料科技有限公司 | 一种石墨烯增强聚甲基丙烯酰亚胺泡沫材料的制备方法 |
| CN106079219A (zh) * | 2016-06-08 | 2016-11-09 | 惠州景华包装制品有限公司 | 一种eps泡沫包装箱生产工艺 |
| CN106079217A (zh) * | 2016-06-08 | 2016-11-09 | 惠州景华包装制品有限公司 | 一种eps红外线预发泡工艺 |
| CN106432592A (zh) * | 2016-09-19 | 2017-02-22 | 浙江中科恒泰新材料科技有限公司 | 一种提高聚甲基丙烯酰亚胺泡沫加工收率的制备方法 |
| CN108084324A (zh) * | 2017-12-27 | 2018-05-29 | 浙江中科恒泰新材料科技有限公司 | 一种高强度异型聚(甲基)丙烯酰亚胺泡沫的制备方法 |
| US10919198B2 (en) | 2015-10-22 | 2021-02-16 | Evonik Operations Gmbh | Production of complex hollow foam or sandwich structures by means of a mold core |
| CN113286686A (zh) * | 2019-01-16 | 2021-08-20 | 赢创运营有限公司 | 制备泡沫材料的新发泡方法 |
| CN113302031A (zh) * | 2019-01-16 | 2021-08-24 | 赢创运营有限公司 | 通过使用微波使含有发泡剂的聚合物发泡 |
Families Citing this family (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4036052C2 (de) * | 1990-11-13 | 1997-05-07 | Roehm Gmbh | Verfahren zur Verminderung von Spannungen in Schaumstoffblöcken aus Polymethacrylimid |
| US5242634A (en) * | 1991-08-06 | 1993-09-07 | Sanwa Kako Company Limited | Method of producing open-cell foams of cross-linked polyolefins |
| DE19639491C2 (de) * | 1996-09-26 | 1999-11-11 | Fraunhofer Ges Forschung | Verfahren zur Vergrößerung der Oberfläche von Partikeln |
| DE102011085026A1 (de) | 2011-10-21 | 2013-04-25 | Evonik Röhm Gmbh | Verfahren zur Herstellung von Korngrenzenhaftung von expandierten Copolymeren auf Basis von Methacryl- und Acrylverbindungen und Anhaftung diverser Deckschichten auf dem Schaumkern |
| DE102013002519B4 (de) | 2013-02-13 | 2016-08-18 | Adidas Ag | Herstellungsverfahren für Dämpfungselemente für Sportbekleidung |
| DE102013205963A1 (de) | 2013-04-04 | 2014-10-09 | Evonik Industries Ag | Verfahren zur kontinuierlichen PMI-Schaumfertigung |
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| DE102016209045B4 (de) | 2016-05-24 | 2022-05-25 | Adidas Ag | Verfahren und vorrichtung zum automatischen herstellen von schuhsohlen, sohlen und schuhe |
| DE102016223980B4 (de) | 2016-12-01 | 2022-09-22 | Adidas Ag | Verfahren zur Herstellung eines Kunststoffformteils |
| DE102017205830B4 (de) | 2017-04-05 | 2020-09-24 | Adidas Ag | Verfahren für die Nachbehandlung einer Vielzahl einzelner expandierter Partikel für die Herstellung mindestens eines Teils eines gegossenen Sportartikels, Sportartikel und Sportschuh |
| CN107325320B (zh) * | 2017-07-21 | 2020-03-24 | 中国工程物理研究院激光聚变研究中心 | 避免聚苯乙烯类空心微球干燥过程开裂的方法 |
| WO2026041546A1 (en) | 2024-08-21 | 2026-02-26 | Evonik Operations Gmbh | Variothermal sintering |
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| DE3372980D1 (en) * | 1983-03-28 | 1987-09-17 | Bayer Ag | Process for preparing polyolefin foams |
| JPS6136534A (ja) * | 1984-07-26 | 1986-02-21 | Mitsuboshi Belting Ltd | Vリブドベルト |
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- 1987-08-27 DE DE8787112433T patent/DE3762324D1/de not_active Expired - Lifetime
- 1987-08-27 ES ES87112433T patent/ES2016601B3/es not_active Expired - Lifetime
- 1987-09-02 US US07/091,970 patent/US4740530A/en not_active Expired - Fee Related
- 1987-09-10 JP JP62225461A patent/JPS6374629A/ja active Pending
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| US3627711A (en) * | 1968-12-27 | 1971-12-14 | Roehm & Haas Gmbh | Foamable synthetic resin compositions |
| GB2134845A (en) * | 1983-02-12 | 1984-08-22 | Roehm Gmbh | Process for producing composite form body |
Cited By (22)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4840758A (en) * | 1988-09-09 | 1989-06-20 | Phillips Petroleum Company | Methods of preparing molded thermoplastic articles wherein radio frequency energy is utilized to heat the thermoplastic material |
| US4990539A (en) * | 1988-12-16 | 1991-02-05 | Basf Aktiengesellschaft | Preparation of styrene polymer foam particles |
| EP0978601A1 (de) * | 1998-08-05 | 2000-02-09 | Exploitatiemaatschappij Merode B.V. | Verfahren und Vorrichtung zur Herstellung eines isolierenden Elementes und damit hergestellter Elemente |
| NL1009885C2 (nl) * | 1998-08-18 | 2000-02-21 | Exploitatiemaatschappij Merode | Werkwijze en inrichting voor het vervaardigen van een isolatie-element, aldus verkregen isolatie-element en dakconstructie voorzien van één of meer isolatie-elementen. |
| EP1332030A4 (de) * | 2000-08-14 | 2009-02-11 | Novamont Spa | Verfahren zum herstellen biologisch abbaubarer schaumprodukte |
| KR100943399B1 (ko) * | 2001-08-29 | 2010-02-22 | 에보니크 룀 게엠베하 | 폴리메타크릴이미드 발포체의 제조방법 및 당해 방법으로 수득 가능한 폴리메타크릴이미드의 발포 판 또는 시이트 |
| US20040101674A1 (en) * | 2002-11-06 | 2004-05-27 | Leslie Ross | Composite sheet material |
| US7208223B2 (en) * | 2002-11-06 | 2007-04-24 | Premium Aircraft Interiors Uk Limited | Composite sheet material |
| CN103524968A (zh) * | 2013-10-23 | 2014-01-22 | 江苏兆鋆新材料科技有限公司 | 一种石墨烯增强聚甲基丙烯酰亚胺泡沫材料的制备方法 |
| US10919198B2 (en) | 2015-10-22 | 2021-02-16 | Evonik Operations Gmbh | Production of complex hollow foam or sandwich structures by means of a mold core |
| CN106079217A (zh) * | 2016-06-08 | 2016-11-09 | 惠州景华包装制品有限公司 | 一种eps红外线预发泡工艺 |
| CN106079219A (zh) * | 2016-06-08 | 2016-11-09 | 惠州景华包装制品有限公司 | 一种eps泡沫包装箱生产工艺 |
| CN106432592A (zh) * | 2016-09-19 | 2017-02-22 | 浙江中科恒泰新材料科技有限公司 | 一种提高聚甲基丙烯酰亚胺泡沫加工收率的制备方法 |
| CN106432592B (zh) * | 2016-09-19 | 2018-07-17 | 浙江中科恒泰新材料科技有限公司 | 一种提高聚甲基丙烯酰亚胺泡沫加工收率的制备方法 |
| CN108084324A (zh) * | 2017-12-27 | 2018-05-29 | 浙江中科恒泰新材料科技有限公司 | 一种高强度异型聚(甲基)丙烯酰亚胺泡沫的制备方法 |
| CN108084324B (zh) * | 2017-12-27 | 2020-11-10 | 浙江中科恒泰新材料科技有限公司 | 一种高强度异型聚(甲基)丙烯酰亚胺泡沫的制备方法 |
| CN113286686A (zh) * | 2019-01-16 | 2021-08-20 | 赢创运营有限公司 | 制备泡沫材料的新发泡方法 |
| CN113302031A (zh) * | 2019-01-16 | 2021-08-24 | 赢创运营有限公司 | 通过使用微波使含有发泡剂的聚合物发泡 |
| JP2022518454A (ja) * | 2019-01-16 | 2022-03-15 | エボニック オペレーションズ ゲーエムベーハー | マイクロ波の使用による発泡剤含有ポリマーの発泡 |
| JP2022518706A (ja) * | 2019-01-16 | 2022-03-16 | エボニック オペレーションズ ゲーエムベーハー | 発泡材料を製造するための新規の発泡法 |
| US11904514B2 (en) | 2019-01-16 | 2024-02-20 | Evonik Operations Gmbh | Foaming process for production of foam materials |
| US12233582B2 (en) | 2019-01-16 | 2025-02-25 | Evonik Operations Gmbh | Foaming of blowing agent containing polymers through the use of microwaves |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0259706A2 (de) | 1988-03-16 |
| ES2016601B3 (es) | 1990-11-16 |
| EP0259706B1 (de) | 1990-04-18 |
| DE3630930A1 (de) | 1988-03-24 |
| DE3762324D1 (de) | 1990-05-23 |
| JPS6374629A (ja) | 1988-04-05 |
| EP0259706A3 (en) | 1988-08-03 |
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